Hydrocarbon-derived resins having low softening point

ABSTRACT

Hydrocarbon resins suitable as tackifiers having softening points in the range of about 25* C. to about 80* C., a volatility of less than about 6 weight percent and a number average molecular weight in the range of about 1000 to about 1400 which comprises from about 5 to about 60 percent units derived from piperylene, from about 1 to about 30 percent units derived from 1,3-butadiene, from about 5 to about 60 percent units derived from isobutylene, from about 5 to about 30 percent units derived from 2-methyl-1-butene, from about 5 to about 40 percent units derived from 2-methyl-2-butene, from about 0 to about 10 percent units derived from isoprene and from about 0 to about 10 percent units derived from other hydrocarbons containing four to six carbon atoms, wherein the ratio of units derived from piperylene to units derived from 1,3-butadiene is from about 10:1 to about 1:2 and the ratio of units derived from piperylene to units derived from isobutylene is from about 6:1 to about 1:6.

United States Patent St. Cyr

1151 3,692,756 [451 Sept. 19,1972

[54] HYDROCARBON-DERIVED RESINS HAVING LOW SOFTENING POINT [72] Inventor: David R. St. Cyr, Uniontown, Ohio [73] Assignee: The Goodyear Tire & Rubber Company, Akron, Ohio [22] Filed: July 2, 1970 21 Appl. No.: 52,133

[52] US. Cl. ..260/80.7, 260/5, 260/82,

260/888, 260/889, 260/894, 260/897 A 51 1m. 01 ..coar 15/40 581 Field of Search ..260/80.7, s2

[56] References Cited UNITED STATES PATENTS 3,509,239 4/1970 Tindall ..260/80.7 3,541,188 11/1970 Srail ..260/82 3,444,259 5/1969 llnyskyj ..260l80.7 3,478,005 1 H1969 Wheeler ..260/80.7 3,467,632 9/1969 Davis ..260I80.7 2,523,150 9/1950 Schneider ..260/82 Primary Examiner-John C. Bleutge Attorney-F. W. Brunner and J. Y. Clo w ey [57] ABSTRACT Hydrocarbon resins suitable as tackifiers having softening points in the range of about 25 C. to about 80 C., a volatility of less than about 6 weight percent and a number average molecular weight in the range of about 1000 to about 1400 which comprises from about 5 to about 60 percent units derived from piperylene, from about I to about 30 percent units derived from 1,3-butadiene, from about 5 to about 60 percent units derived from isobutylene, from about 5 to about 30 percent units derived from 2-methyl-l butene, from about 5 to about 40 percent units derived from Z-methyI-Z-butene, from about 0 to about 10 percent units derived from isoprene and from about 0 to about 10 percent units derived from other hydrocarbons containing four to six carbon atoms, wherein the ratio of units derived from piperylene to units derived from 1,3-butadiene is from about 10:1 to about 1:2 and the ratio of units derived from piperylene to units derived from isobutylene is from about 6:1 to about 1:6.

6 Claims, No Drawings HYDROCARBON-DERIVED RESINS HAVING LOW SOFTENING POINT mixing low molecular weight oils with high softening" point resins. Typically, the selected hydrocarbon mixtures are polymerized with Friedel-Crafts catalysts to form resins having low molecular weights in the range of about 300 to about 800 or an oil having a low molecular weight in the range of about 300 to about 500 is mixed with a resin having a high softening point of about 90 C. to about 120 C. and a molecular weight in the range of about 1200 to about 2000 to prepare the low softening point resins.

Hydrocarbon-derived resins having low molecular weights and low softening points are typically accompanied with too high a volatility and thus unsuitable as tackifiers for most polymers. Volatility is detrimental to applications of resins in areas of heat exposure.

The mixing of a low molecular weight oil with a high softening point resin having good tackifying properties is generally disadvantageous since it typically dilutes and thus reduces the tackifying properties of the resin and also greatly increases its volatility due to the low molecular weight oil being present, rendering it unsuitable for many commercial applications.

Therefore, it is an object of this invention to provide hydrocarbon-derived resins having low softening points while maintaining good tackifying properties, moderate molecular weights and low volatility.

It is known that, in the presence of Friedel-Crafts type of catalysts, piperylene typically produces polymers which have little or no commercial value because their physical properties render them generally unsuitable for use in commercial applications. lsobutylene typically polymerizes with such catalysts at about C. to about 30 C. only very slowly to ultimately produce rubbery polymers, although it can be polymerized under more stringent conditions, to give a resin with a molecular weight in the range of 300 to 1900, a softening point of less than about 50 C., but generally with too high a volatility. With such catalysts l,3-butadiene typically produces low molecular weight gummy materials. Attempting to polymerize 2-methyll-butene, 2-methyl-2-butene or B-mcthyl-l-butehe with Friedel-Crafts catalysts has typically resulted in no polymer at all, or at the most, low molecular weight oily products.

Thus, it is a further object of this invention to provide new and useful resinous polymers having tackifying properties comprising units derived primarily from piperylene, 1,3-butadiene, isobutylene, 2-methyl-l-butene, 2-rnethyl-2-butene and isoprene. It is an additional object to provide a method of preparing such resinous polymers. In the practice of this invention, the term piperylene is used to refer to a mixture of cisl,3 and trans-1,3 pentadienes typically containing from about 30 to about 70 weight percent trans-1,3-pentadiene, and correspondingly,.about 70 to about 30 weight percent cis-l ,3-pentadiene.

ln practice, this invention is desirably accomplished by selectively mixing and polymerizing varying portions of at least two hydrocarbon mixtures, hereinafter identified as Mixture A and Mixture B. By suitable choice of proportions of these mixtures, the required hydrocarbon-derived resins are produced having low softening points according to ASTM Test E28-58T in the range of from about 25 C. to about 80 C., a low volatility of less than about 6 weight percent, and relatively high molecular weights of a number average in the range of from about 1000 to about 1400 while still maintaining good tackifying properties.

It was discovered that it is a characterization of this method that the resin softening point is substantially directly proportional to the weight ratio of Mixtures A and B when the compositions of each of the said mixtures is held substantially constant. This substantially straight line relationship was observed when Mixture A was in the range of about 25 to about 85 weight percent and Mixture B was in the range of about 15 to about 75 weight percent of the total monomer mixture.

For the accomplishment of this invention, hydrocarbon Mixture A comprises from about 25 to about 60 weight percent of isobutylene, from about 5 to about 30 weight percent 1,3-butadiene, from about 5 to about 35 weight percent 2-methyl-l-butene, from about 0 to about l0 weight percent isoprene, and from about 0 to about 15 weight percent of other hydrocarbons containing from four to five carbon atoms.

For this invention, Mixture B comprises from about 20 to 50 weight percent 2-methyl-2-butene, from about 20 to 60 weight percent piperylene, from about 2 to 20 weight percent 4-methyl-2-pentene, from about 0 to 5 weight percent isoprene, from about 0 to 15 weight percent of other hydrocarbons containing five to six carbon atoms and from about 0 to 10 weight percent of dimers and codimers of unsaturated hydrocarbons containing five to six carbon atoms having boiling points above C.

The resins of this invention have the composition and structure of resins which comprise from about 25 to about 85 percent units derived from hydrocarbon Mixture A and from about 15 to about percent units derived from hydrocarbon Mixture B. They are useful as tackifiers and extenders for natural rubber and various synthetic rubbers. The resins are typically characterized by having a volatility of from about l to about 6 weight percent as measured by oven aging for five hours at 350 F. or 177 C. when the resins are recovered and finished by vacuum distillation. if the resins are finished by steam stripping, they typically have a volatility of from about 1 to about 3 weight percent.

Thus, according to this invention, it has been discovered that a resinous polymer useful as a tackifier and having a softening point of from about 25 C. to about C., a molecular weight of about 1000 to about I400 and a volatility of from about l to about 6 weight percent, comprises from about 5 to about 60 percent units derived from piperylene, from about I to about 20 percent units derived from 1,3-butadiene, from about 5 to about 60 percent units derived from isobutylene, from about 5 to about 30 percent units derived from Z-methyl-l -butene, from about 5 to about 40 percent units derived from Z-methyl-Z-butene,

about zero to about 10 percent units derived from isoprene, and from about zero to about 10 percent units derived from other hydrocarbons containing four to six carbon atoms, wherein the ratio of units derived from piperylene to units derived from 1,3 -butadiene is from about 10:1 to about 1:2 and the ratio of units derived from piperylene to units derived from isobutylene is from about 6:1 to about 1:6. Thus, controlled mixtures of unsaturated hydrocarbons containing four to six carbon atoms which, on an individual basis, typically produce products with comparatively limited commercial value, are subjected to polymerization conditions to produce low softening point resinous polymers having low volatility and useful tackifying properties.

In the practice of this invention, the resinous polymer is prepared by subjecting to polymerization in the presence of an anhydrous catalyst selected from aluminum chloride and ethyl-aluminum dichloride, a mixture comprising from about 20 to about 60 weight percent piperylene, from about to about 30 weight percent 1,3-butadiene, from about 25 to about 75 weight percent isobutylene, from about 5 to about 35 weight percent Z-methyl-l-butene, from about 20 to about 50 weight percent 2-methyl-2-butene, from about zero to about 15 weight percent 3-methyl-l-butene, from about 0 to about weight percent isoprene, and from about zero to about weight percent of other hydrocarbons having four to six carbon atoms.

In carrying out the polymerization, the mixture of monomers can be contacted with the catalyst by various means. The catalyst may be added to the monomer mixture or the monomer mixture may be added to the catalyst. If desired, the catalyst and mixture of monomers may be added simultaneously or intermittently to a reactor. The reaction can be conducted continuously or by batch process techniques generally known to those skilled in the art. When a particulate catalyst is used typically it has a particle size in the range of from about 5 to about 200 U. S. Standard mesh size, although larger or smaller particles can be used. Although the amount of catalyst is not critical, a sufficient amount of catalyst is used to cause a polymerization reaction to occur.

The reaction is conveniently carried out in the presence of a diluent because it is usually exothermic. However, with adequate mixing and cooling, the temperature can be controlled and the reaction conducted without a diluent. Various diluents which are inert in that they do not enter into the polymerization may be used. Representative examples are aliphatic hydrocarbons such as pentane, hexane and heptane, dichloromethane, aromatic hydrocarbons, such as toluene, benzene and unreacted residual hydrocarbons from the reaction.

A wide range of temperatures can be used for the polymerization reaction. The polymerization can be carried out at temperaturesin the range of from about 30 C. to about 100 C., although usually the reaction is carried out at a temperature in the range of from about C. to about 50 C. The polymerization reaction pressure is not critical and may be atmospheric or above or below atmospheric pressure. Generally, a satisfactory polymerization can be conducted when the reaction is carried out at about autogenous pressure developed by the reactor under the operating conditions used. The time of the reaction is not generally critical and reaction times can vary from a few seconds to 12 hours or more.

The resinous compositions of this invention are generally soluble in aliphatic hydrocarbons such as pentane, hexane and heptane and aromatic hydrocarbons such as benzene and toluene. They are generally useful as modifiers for natural rubber and various synthetic rubbers. They are particularly useful in hot melts.

The following examples further illustrate the invention and are not intended to be limiting. In these examples, parts and percentages are by weight unless otherwise indicated.

EXAMPLE I Two streams (A and B) having thefollowing compositions were blended to give a monomer mixture consisting of 50 parts of Stream A and 50 parts of Stream Stream f Piperylenes 39.8 lsoprene and cyclopentene 6.6 Other hydrocarbons having 5 to 6 carbon atoms 10.7

Into a reactor purged with nitrogen and fitted with a stirrer, dry ice jacketed addition funnel, condenser, dry ice cold finger, and nitrogen purging system, was placed 600 parts of dichloromethane and 44 parts of anhydrous particulate aluminum chloride. The mixture was adjusted to a temperature of about 8 C. to -l2 C. To the reaction was slowly charged 2420 parts of the hydrocarbon mixture containing 1210 parts of Stream A and 1210 parts of Stream B over a period of about 4% hours. After addition, the mixture was stirred for an additional A hour. The resulting mixture was filtered through a Celite-asbestos filter bed and then distilled to a pot temperature of about 200 C. under a nitrogen atmosphere. Steam at 250 C. was added and the pot temperature allowed to go to 235 C. The pot temperature was held at 235 C. until the water to oil ratio in the distillate was 20 to 1. The hot resin was poured into aluminum pans to cool. The yield was 68.2 percent of an opaque yellow resinous material having a softening point of about 53 C. according to ASTM Method E28-58T. The resin had an average molecular weight of l l 10, as determined by vapor pressure osmometry. A sample of the resin was heated for five hours at 350 F. or 177 C., in an air circulating oven with a resultant ComP Perm" weight loss of 1.87 percent, thus exhibiting a volatility 5 of only 2 weight percent. Z-methyI-Z-butene 42.5

A material balance around the reaction system in- F 4-methyl-cis-2-pentene 26.9 dicated the resulting resinous material to have the folm5 lowing composition: Other hydrocarbons with boiling points above 70 C. 8.0

Other hydrocarbons with from Comp und Pe en s to 6 carbon atoms 6.l

lsobutylene l 8.7 into a reactor, purged with nitrogen and fitted with a Z-methyl-l-butene stirrer, dry ice jacketed dripping funnel, condenser, dry g y ice cold finger, and nitrogen purge system, was placed ipery ene o i I other hydrocarbons having 100 parts of dichloromethane and 8 parts of anhydrous 4 to 6 carbon atoms 7.9 particulate aluminum chloride. The mixture was ad- 2O justed to a temperature of about -5 C. to l5 C. To

EXAMPLE ll The two streams (A and B) used in Example I were blended to give a monomer mixture consisting of 30 percent Stream A and 70 percent Stream B. The equipment and reaction procedure used was the same as in Example 1. The monomer mixture consisted of 660 parts of Stream A and 1540 parts of Stream B. After distillation, the yield was 71.1 percent of an opaque yellow resinous material having a softening point of about 72 C. and an average molecular weight of 1130. A sample of the resin was heated for five hours at 350 F. or 177 C. in an air circulating oven with a resultant weight loss of 1.78 percent (a volatility of less than 2 percent). A material balance around the reaction system indicates the resulting resinous material to have the following composition:

Percent Two streams (A and B) having the following compositions were blended to give a monomer mixture consisting of 75 parts of Stream A and parts of Stream B.

Stream A Compound Percent Isobutylene Trans-Z-butcne Cis-Z-butene l ,3butadiene Z-methyl-l-butene 3-methyl-l-butcne Other hydrocarbons having from 4 to 5 carbon atoms Stream B the reactor was slowly charged 400 parts of a hydrocarbon monomer mixture made up of 300 parts of Stream A and 100 parts of Stream B over a period of about one hour. After the addition, the mixture was stirred for another hour. Then 15.8 parts of isopropanol and l0 parts of water was added to deactivate the catalyst. The resulting mixture was filtered through an asbestos- Celite filter bed and then distilled to a pot temperature of about 250 C. at a reduced pressure of about 10 millimeters of mercury. The hot resin in the pot was poured onto a glass surface and cooled to about 25 C. to form a yield of 58 percent of an opaque yellow resinous material having a softening point of about 25 C. according to ASTM Method E28-'-58T. The resin had a molecular weight of l080 as determined by vapor pressure osmometry. After heat again in an air circulating oven for five hours at 350 F. the resultant weight loss was 4.02 percent.

EXAMPLE IV The two streams (A and B) used in Example lll were blended to give a monomermixture of 50 percent Stream A and 50 percent Stream B. The equipment and reaction procedure used was the same as in Example ll]. The monomer mixture consisted of 200 parts Stream A and 200 parts Stream B. After distillation the yield was 51 percent of an opaque yellow resinous material having a softening point of 47 C. and a molecular weight of 1090. A sample of the resin was heated for five hours at 350 F. in an air circulating oven with a resultant weight loss of 5.03 percent.

EX AM PLE V The two streams (A and B) used in Example Ill were blended to give a monomer mixture of 25 percent Stream A and percent Stream B. The equipment and reaction procedure used was the same as in Example Ill. The monomer mixture consisted of parts of Stream A and 300 parts of Stream B. After distillation, the resinous material had a softening point of about 68 C. and a molecular weight of 1070. A sample of the resin was heated for five hours at 350 F. in an air circulating oven with a resultant weight loss of 4.4 percent.

The softening points of the resins prepared in Examples lll, IV and V, when plotted versus the ratios of Streams A and B, demonstrate the substantially direct relationship therebetween by the relatively straight line. The softening points are in the range of 25C. and 68 C. and the ratio of A to B ranges from 75:25 to 25:75. Certainly it should also be observed that the volatility ranges from 2 percent to 5 percent and the average molecular weight was in the narrow range of 1070 to 1090.

The resins required in this invention and as specifically exemplified in these examples are suitable tackifiers for various polymers such as natural and synthetic rubber, and such compositions comprise from about 5 to about 50 parts by weight of the resin per 100 parts by weight of polymer. The compositions are suitable as pressuresensitive adhesives, particularly with the higher resin loadings. Representative of various synthetic rubbers are rubbery polymers of conjugated dienes including polybutadiene, polyisoprene, copolymers of butadiene and isoprene which contain a major portion of butadiene, particularly copolymers of butadiene and styrene of the hot and cold SBR type which contain from about 60 to about 80 percent by weight of butadiene, copolymers of butadiene and acrylonitrile,-butyl rubber, which is a polymerization product of a major portion of a monoolefin such as isobutylene and a minor portion of a diolefin, such as butadiene or isoprene, co-polymers of ethylene and propylene and terpolymers of ethylene, propylene and a diene.

The resins required by this invention and a specifically exemplified in the examples are suitable as tackifiers in hot melt compositions. Such hot melt compositions comprise from about to about 40 parts by weight of the resin per 100 parts by weight of at least one thermoplastic polymer selected from the group consisting of polyethylene having a molecular weight of from about 1500 to about 21,000, atactic polypropylene, polybutene and ethylene-vinyl acetate copolymers.

While certain representative embodiments and details have been shown for the purpose of illustrating the invention, it will be apparent to those skilled in this art that various changes and modifications may be made therein without departing from the spirit or scope of the invention.

What is claimed is:

l. A hydrocarbon-derived resin suitable as a tackifier having a softening point in the range of from about 25 C. to about 80 C., a volatility of less than about 6 weight percent and a number average molecular weight in the range of about 1000 to about 1400 which comprises from about 5 to about 60 percent units derived from piperylene, from about 1 to about 30 percent units derived from 1,3-butadiene, from about 5 to about 60 percent units derived from isobutylene, from about StoYa tbout 30 percent units derived from 2- methyl-l -bute ne, from about 5 to about 40 percent units derived from 2-methyl-2-butene, from about 0 to about 10 percent units derived from isoprene and from about 0 to about 10 percent-units derived from other hydrocarbons containing four to six carbon atoms, wherein the ratio of units derived from piperylene to units derived from 1,3-butadiene is from about 10:1 to about 1:2 and theratio of units derived from piperylene to units derived from isobutylene is from about 6:1 to

about 1:6 prepared by the method which comprises polymerizing a hydrocarbon mixture of the composition prepared by mixing from about 25 to about 85 weight percent of Mixture A with from about 15 to about 75 weight percent of Mixture B, at a temperature of from about -20 C. to about 50 C., in the presence of an anhydrous catalyst selected from aluminum chloride and ethylaluminum dichloride wherein it is a characterization of the said method that the resin softening point is substantially directly proportional to the weight ratio of Mixtures A and B when the compositions of each of the said Mixtures is held substantially constant where Mixture A comprises from about 25 to about 60 weight percent isobutylene, from about 5 to about 30 weight percent l,3-butadiene, from about 5 to about 35 weight percent 2-methyl-lbutene, from about 0 to about 10 weight percent isoprene, and from about 0 to about 15 weight percent of other hydrocarbons containing four to five carbon atoms, and where Mixture B comprises from about 20 to about 50 weight percent 2-methyl-2-butene, from about 20 to 60 weight percent piperylene, from about 0 to 5 weight percent isoprene, from about 0 to 15 weight percent of other hydrocarbons containing five to six carbon atoms and from about 0 to 10 weight percent of dimers and codimers of unsaturated hydrocarbons containing five to six carbon atoms having boiling points above C.

2. The hydrocarbon-derived resin according to claim 1 having a volatility in the range of about 1 to about 3 weight percent as measured by aging for about five hours at 177 C.

3. The hydrocarbon-derived resin according to claim 1 having a volatility in the range of about 1 to about 6, where the method comprises polymerizing the hydrocarbon mixture in the presence of an inert diluent and where the said anhydrous catalyst is aluminum chloride having a particular size in the range of about 5 to about 100 US. Standard mesh size.

4. The method of preparing the hydrocarbon-derived resin of claim 1 which comprises polymerizing a hydrocarbon mixture containing from about 25 to about 85 weight percent of Mixture A and from about 15 to about weight percent of Mixture B, at a temperature of from about 20 C. to about 50 C., in the presence of an anhydrous catalyst selected from aluminum chloride and ethylaluminum dichloride wherein it is a characterization of the said method that the resin softening point is substantially directly proportional to the weight ratio of Mixtures A and B when the compositions of each of the Mixtures is held substantially constant where Mixture A comprises from about 25 to about 60 weight percent isobutylene, from about 5 to about 30 weight percent 1,3-butadiene, from about 0 to about 35 weight percent 2-methyl-l-butene, from about 0 to about 10 weight percent isoprene, and from about 0 to about 15 weight percent of other hydrocarbons containing four to five carbon atoms, where Mixture B comprises from about 20 to 50 weight percent 2- methyl-2-butene, from about 20 to 60 weight percent piperylene, from about 2 to 20 weight percent 4- methyl-Z-pentene, from about 0 to 5 weight percent isoprene, from about 0 to 15 weight percent of other hydrocarbons containing five to six carbon atoms and from about 0 to 10 weight percent of dimers and codimers of unsaturated hydrocarbons containing five .19 polymerization is conducted in the presence of an inert diluent and where the anhydrous catalyst is in the range of about 5 to about l00 U.S. Standard mesh size.

6. The hydrocarbon-derived resin according to claim 1 where the anhydrous catalyst is aluminum chloride.

a a: a a: 

2. The hydrocarbon-derived resin according to claim 1 having a volatility in the range of about 1 to about 3 weight percent as measured by aging for about five hours at 177* C.
 3. The hydrocarbon-derived resin according to claim 1 having a volatility in the range of about 1 to about 6, where the method comprises polymerizing the hydrocarbon mixture in the presence of an inert diluent and where the said anhydrous catalyst is aluminum chloride having a particular size in the range of about 5 to about 100 U.S. Standard mesh size.
 4. The method of preparing the hydrocarbon-derived resin of claim 1 which comprises polymerizing a hydrocarbon mixture containing from about 25 to about 85 weight percent of Mixture A and from about 15 to about 75 weight percent of Mixture B, at a temperature of from about -20* C. to about 50* C., in the presence of an anhydrous catalyst selected from aluminum chloride and ethylaluminum dichloride wherein it is a characterization of the said method that the resin softening point is substantially directly proportional to the weight ratio of Mixtures A and B when the compositions of each of the Mixtures is held substantially constant where Mixture A comprises from about 25 to about 60 weight percent isobutylene, from about 5 to about 30 weight percent 1,3-butadiene, from about 0 tO about 35 weight percent 2-methyl-1-butene, from about 0 to about 10 weight percent isoprene, and from about 0 to about 15 weight percent of other hydrocarbons containing four to five carbon atoms, where Mixture B comprises from about 20 to 50 weight percent 2-methyl-2-butene, from about 20 to 60 weight percent piperylene, from about 2 to 20 weight percent 4-methyl-2-pentene, from about 0 to 5 weight percent isoprene, from about 0 to 15 weight percent of other hydrocarbons containing five to six carbon atoms and from about 0 to 10 weight percent of dimers and codimers of unsaturated hydrocarbons containing five to six carbon atoms having boiling points above 70* C. and where the produced resin contains a ratio of units derived from piperylene to units derived from 1,3-butadiene of about 10:1 to about 1:2 and a ratio of units derived from piperylene to units derived from isobutylene of from about 6:1 to about 1:6.
 5. The method according to claim 4 where the polymerization is conducted in the presence of an inert diluent and where the anhydrous catalyst is in the range of about 5 to about 100 U.S. Standard mesh size.
 6. The hydrocarbon-derived resin according to claim 1 where the anhydrous catalyst is aluminum chloride. 